DE973134C - Process for the production of dimensionally stable porous moldings from thermoplastics - Google Patents

Process for the production of dimensionally stable porous moldings from thermoplastics

Info

Publication number
DE973134C
DE973134C DEB14755A DEB0014755A DE973134C DE 973134 C DE973134 C DE 973134C DE B14755 A DEB14755 A DE B14755A DE B0014755 A DEB0014755 A DE B0014755A DE 973134 C DE973134 C DE 973134C
Authority
DE
Germany
Prior art keywords
production
dimensionally stable
thermoplastics
moldings
porous moldings
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
DEB14755A
Other languages
German (de)
Inventor
Fritz Dr Stastny
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Priority to DEB14755A priority Critical patent/DE973134C/en
Priority to US282682A priority patent/US2779062A/en
Priority to FR1055058D priority patent/FR1055058A/en
Priority to GB10297/52A priority patent/GB719729A/en
Application granted granted Critical
Publication of DE973134C publication Critical patent/DE973134C/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/16Making expandable particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/38Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
    • B29C44/44Feeding the material to be shaped into a closed space, i.e. to make articles of definite length in solid form
    • B29C44/445Feeding the material to be shaped into a closed space, i.e. to make articles of definite length in solid form in the form of expandable granules, particles or beads
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/22After-treatment of expandable particles; Forming foamed products
    • C08J9/228Forming foamed products
    • C08J9/232Forming foamed products by sintering expandable particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3415Heating or cooling
    • B29C44/3426Heating by introducing steam in the mould

Description

Verfahren zur Herstellung maßhaltiger poröser Formkörper aus thermoplastischen Kunststoffen Es ist bekannt, aus thermoplastischen Kunststoffen und Treibmitteln, d. h. Verbindungen, die sich beim Envärmen unter Gasbildung zersetzen, poröse Formkörper herzustellen. Dazu werden die zerkleinerten Kunststoffe mit Treibmitteln vermischt und in gasdichten Formen unter Erwärmung auf die Erweichungstemperatur des Kunststoffes zu Formkörpern verpreßt, wobei gleichzeitig die Zersetzung der Treibmittel stattfindet. Diese Formkörper werden dann nach dem Abkühlen aus der Preßform entnommen und nochmals bis zum Erweichen erwärmt. Dabei werden durch die unter Druck stehenden, durch die Zersetzung der Treibmittel entstandenen Gase die porösen Körper gebildet. Durch dieses Verfahren gelingt es, Körper von verhältnismäßig einfacher Gestalt, z. B. Platten, Kugeln u. dgl., herzustellen. Es versagt aber, wenn man kompliziertere Formkörper, z. B. Puppen oder Tierfiguren, erzeugen will, da beim Aufschäumen derartiger Preßkörper ungleichmäßige Formveränderungen auftreten.Process for the production of dimensionally stable porous moldings from thermoplastic Plastics It is known from thermoplastics and blowing agents, d. H. Compounds that decompose with gas formation when heated, porous moldings to manufacture. For this purpose, the shredded plastics are mixed with propellants and in gas-tight forms with heating to the softening temperature of the plastic pressed into moldings, the decomposition of the blowing agent taking place at the same time. These moldings are then removed from the mold after cooling and again warmed until softened. The pressurized, the Decomposition of the propellant resulting gases formed the porous body. By this method succeeds in body of relatively simple shape, z. B. Plates, balls and the like. To produce. But it fails when you get more complicated Molded body, e.g. B. dolls or animal figures want to produce, as such when foaming Pressed body uneven changes in shape occur.

Die gleichen Nachteile besitzt ein aus der belgischen Patentschrift 496 635 bekanntes Verfahren, bei dem zerkleinerte Kunststoffe, die auch Lösungs-oder Weichmachungsmittel enthalten können, in Formen in Gegenwart von unter Druck stehenden Gasen erwärmt werden. Es entstehen hierbei gashaltige Formkörper, die nach dem Abkühlen und Entnehmen aus den Formen durch Erwärmen aufgeschäumt werden. One from the Belgian patent specification has the same disadvantages 496 635 known process in which shredded plastics, which are also solvent or Plasticizers may contain, in forms in the presence of pressurized Gases be heated. This results in gas-containing moldings, which after cooling and removing from the molds are foamed by heating.

Die Erfindung besteht darin, daß man zur Herstellung von maßhaltigen, porösen Formkörpern aus zerkleinerten thermoplastischen Kunststoffen in Gegenwart von Blähmitteln zerkleinerte thermoplastische Kunststoffe, die Gase gelöst enthalten, in nicht gasdicht schließende Formen einbringt und dort durch Erwärmen auf Temperaturen oberhalb des Erweichungspunktes der Kunststoffe zu porösen Formkörpern versintert. The invention consists in that for the production of dimensionally stable, porous moldings made of crushed thermoplastics in the presence thermoplastics that have been shredded by blowing agents and contain dissolved gases, introduces into non-gastight molds and there by heating to temperatures sintered to form porous moldings above the softening point of the plastics.

Bei der Durchführung des Verfahrens muß darauf geachtet werden, daß die verwendete Kunststoffmenge ausreichend zur Erzeugung eines tYberdruckes in der Form ist, um eine einwandfreie Verbindung der einzelnen Kunststoffteilchen zu gewährleisten. When carrying out the procedure, care must be taken that the amount of plastic used is sufficient to generate excess pressure in the Shape is to ensure a perfect connection of the individual plastic particles.

Die Herstellung der gashaltigen Kunststoffmassen, die in zerkleinerter Form zu porösen Formkörpern aufgeschäumt werden, kann nach verschiedenen Verfahren erfolgen. So kann man beispielsweise Mischungen aus Kunststoffen und Treibmitteln in geschlossenen Formen, gegebenenfalls unter Druck, über den Erweichungspunkt der Kunststoffe und die Zersetzungstemperatur der Treibmittel erwärmen und nach dem Abkühlen zerkleinern. Man kann aber auch Kunststoffschmelzen mit indifferenten Gasen unter hohem Druck behandeln, abkühlen lassen und zerkleinern. The production of the gaseous plastic mass, which is crushed in Form to be foamed into porous moldings, can be according to various methods take place. For example, you can use mixtures of plastics and propellants in closed molds, if necessary under pressure, above the softening point of the Heat plastics and the decomposition temperature of the propellants and after that Chop up cooling. But you can also melt plastic with inert gases Treat under high pressure, allow to cool and chop.

Es ist ferner möglich, zerkleinerte Kunststoffe mit verflüssigten oder verfestigten Gasen, z. B. flüssiger Luft oder fester Kohlensäure, zu mischen und in Druckformen zu erwärmen und nach dem Abkühlen die gashaltigen Kunststoffmassen zu zerkleinern.It is also possible to use crushed plastics with liquefied or solidified gases, e.g. B. liquid air or solid carbon dioxide to mix and to heat them in printing forms and, after cooling, the gaseous plastic masses to shred.

Zur Ausführung des Verfahrens sind praktisch alle thermoplastischen Kunststoffe geeignet, insbesondere aber Polyvinylverbindungen, z. B. Polystyrol, Polyvinylchlorid, Polyvinylidenchlorid, Polyvinylcarbazol, Polyvinylester organischer Säuren, Polyacrylsäure- und Polymethacrylsäureverbindungen sowie Mischpolymerisate der genannten Vinylderivate, ferner Polyamide, Polyurethane und andere thermoplastische Polykondensationsprodukte. Practically all of them are thermoplastic to carry out the process Plastics suitable, but especially polyvinyl compounds, e.g. B. polystyrene, Polyvinyl chloride, polyvinylidene chloride, polyvinyl carbazole, polyvinyl ester organic Acids, polyacrylic acid and polymethacrylic acid compounds and copolymers of the vinyl derivatives mentioned, as well as polyamides, polyurethanes and other thermoplastics Polycondensation products.

Als Treibmittel kann man beispielsweise Bicarbonate, Azoverbindungen oder Hydrazinverbindungen verwenden. Durch die Höhe des Treibmittelzusatzes kann der Gasgehalt der Kunststoffmassen. auf die jeweiligen Erfordernisse eingestellt werden. Den Kunststoffmassen können verschiedenartige Zusatzstoffe, wie Farbstoffe, Weichmacher, Pigmente, unbrennbare Stoffe oder beim Verbrennen unbrennbare Gase abgebende Stoffe u. dgl., beigemischt werden.Bicarbonates, azo compounds, for example, can be used as blowing agents or use hydrazine compounds. The amount of propellant added can the gas content of the plastic mass. adjusted to the respective requirements will. Various additives, such as dyes, Plasticizers, pigments, incombustible substances or, if burned, incombustible gases emitting substances and the like., are added.

Beim Aufschäumen der gashaltigen Kunststoffteilchen muß die Eigenart des betreffenden Kunststoffes berücksichtigt werden. So kann man z.B. bei Verarbeitung von gashaltigen Polystyrolteilchen den Schäumungsvorgang besonders vorteilhaft in heißem Wasser oder Wasserdampf von über 100 bis 1400C oder in etwa 100 bis I300C warmem Glycerin oder auch durch Erwärmen mit Infrarotstrahlen oder Heißluft vornehmen. Die Aufschäumung von gashaltigen Teilchen auf Basis von z. B. Polyamiden erfolgt zweckmäßig in heißen Kohlenwasserstoffen. When foaming the gas-containing plastic particles, the peculiarity of the plastic concerned must be taken into account. So you can, for example, when processing of gas-containing polystyrene particles, the foaming process is particularly advantageous in hot water or steam of over 100 to 1400C or around 100 to I300C warm glycerine or by heating with infrared rays or hot air. The foaming of gas-containing particles based on z. B. polyamides useful in hot hydrocarbons.

Das spezifische Gewicht der hergestellten maßhaltigen Formkörper kann innerhalb weiter Grenzen schwanken. Im allgemeinen gelingt es, poröse Formkörper vom spezifischen Gewicht o,6 bis 0,02 und noch weniger herzustellen. Die porösen Formkörper lassen sich auch mechanisch nachbearbeiten, z. B. durch Zersägen, Abdrechseln u. dgl. Sie können auf den verschiedensten Gebieten verwendet werden, insbesondere aber als Isoliermaterialien in der Wärme- und Kältetechnik, als Korkersatz allgemein, als Schwimmkörper, Holzaustauschprodukte, Leichtstoffe aller Art, als Spielsachen, z. B. The specific weight of the dimensionally stable moldings produced can fluctuate within wide limits. In general, porous moldings are possible with a specific gravity of 0.6 to 0.02 and even less. The porous Shaped bodies can also be reworked mechanically, e.g. B. by sawing, trimming and the like They can be used in various fields, in particular but as insulating materials in heating and cooling technology, as a cork substitute in general, as floats, wood replacement products, light materials of all kinds, as toys, z. B.

Tierfiguren, Puppen, Puppenköpfe, als Isoliermaterial in der Elektrotechnik, insbesondere zur Erzeugung von bandartigem geschäumtem Material, das zur Umhüllung für Drähte verwendet werden kann, ferner für Dichtungen, zur Herstellung von Flaschenkorken Kronenkorkscheiben, Dichtungsplättchen, Schwimmgürtelteilen, Rettungsringen.Animal figures, dolls, doll heads, as insulating material in electrical engineering, in particular for the production of ribbon-like foamed material that is used for wrapping can be used for wires, also for seals, for the production of bottle corks Crown cork washers, sealing plates, swim belt parts, lifebuoys.

Booten und Bootsteilen, Diaphragmen, Schuhen und Schuhteilen, Wandplatten, Fußbodenbelägen, Tischplatten, Verpackungsdosen und sonstigen Verpackungskörpern, Lampenschinnen und sonstigen Formkörpern, die sich neben einer relativ hohen Festigkeit durch ein sehr niedriges spezifisches Gewicht auszeichnen.Boats and boat parts, diaphragms, shoes and shoe parts, wall panels, Floor coverings, table tops, packaging cans and other packaging items, Lamp chutes and other moldings, which in addition to a relatively high strength characterized by a very low specific weight.

Beispiel I 850 Teile Polystyrol werden mit I50 Teilen Ammoniumbicarbonat in einer Kugelmühle fein vermahlen und das Gemisch dann in eine gasdichte zylindrische Druckform, die an den beiden Enden mit Schraubdeckeln abgeschlossen wird, eingeführt und auf I800 C erwärmt. Nach Stündigem Erhitzen wird auf 250 C abgekühlt und aus der Form ein gashaltiger Festkörper entnommen, der durch Vermahlen in einer Schlagkreuzmühle auf Korngröße zerkleinert wird. 30 g des zerkleinerten Materials werden in eine eiserne Puppen-Negativform mit einem Volumen von I50 cm3, die an einigen Stellen perforiert ist bzw. Luftlöcher aufweist, eingeführt, hierauf 45 Minuten in 950 C warmes Wasser getaucht und sodann abgekühlt. Man erhält eine sehr schlagfeste formgerechte und maßhaltige Puppe vom spezifischen Gewicht 0.2. Example I 850 parts of polystyrene are mixed with 150 parts of ammonium bicarbonate finely ground in a ball mill and then pour the mixture into a gas-tight cylindrical Printing form, which is closed at both ends with screw caps, introduced and heated to 1800 C. After hours of heating, the mixture is cooled to 250 ° C. and off a gaseous solid is removed from the mold, which is then milled in a cross beater mill is crushed to grain size. 30 g of the crushed material are put into a iron doll negative form with a volume of 150 cm3, which in some places is perforated or has air holes, introduced, then 45 minutes at 950 ° C dipped in warm water and then cooled. You get a very impact-resistant form-fitting and dimensionally stable doll with a specific weight of 0.2.

Beispiel 2 Gekörntes Polystyrol wird in ein offenes Gefäß eingebracht und dieses Gefäß in ein Druckgefäß eingeführt und dort bei 2ooP C der Einwirkung eines Druckes von 500 Atmosphären Stickstoff für die Dauer von I50 Minuten ausgesetzt. Man kühlt ab und zerkleinert den erhaltenen Festkörper. 200 g des zerkleinerten, gashaltigen Polystyrols werden in eine Form von den Dimensionen 500.400i0o mm. die an einzelnen Stellen Durchlochungen aufweist. eingebracht. Man behandelt nun 2 Stunden mit Wasserdampf von IIoO C und kühlt ab. Es wird eine maßhaltige poröse Platte vom spezifischen Gewicht 0,I erhalten. Example 2 Grained polystyrene is placed in an open vessel and this vessel is introduced into a pressure vessel and there at 2ooP C of the action exposed to nitrogen pressure of 500 atmospheres for 150 minutes. It is cooled and the solid obtained is comminuted. 200 g of the crushed, The gaseous polystyrene is made into a mold with the dimensions 500,400i0o mm. the has perforations at individual points. brought in. The treatment is now carried out for 2 hours with Water vapor from IIoO C and cools down. It will be true to size porous plate of specific gravity 0.1 obtained.

Beispiel 3 8 5 o Teile Polymethacrylsäuremethylester werden mit I50 Teilen Azodibuttersäurediisonitril in einer Kugelmühle fein vermahlen. Das Gemisch wird sodann in einer gasdichten Druckform ohne Anwendung eines äußeren Druckes 2 Stunden auf IsoO C erwärmt. Man läßt abkühlen und entnimmt einen homogenen Festkörper, der anschließend durch Vermahlen zerkleinert wird. I00 g dieses zerkleinerten Materials werden dann in eine verschließbare Kugelform mit einem Volumen von looo cm3 eingebracht und 60 Minuten der Einwirkung von Wasserdampf bei 1 100 C ausgesetzt. Man erhält nach dem Abkühlen und Entformen einen kugelförmigen porösen Formkörper vom spezifischen Gewicht O,I. Example 3 8 5 o parts of methyl polymethacrylate are mixed with 150 Grind parts of azodibutyric acid diisonitrile finely in a ball mill. The mixture is then in a gas-tight printing form without the application of external pressure 2 Heated to IsoO C for hours. It is allowed to cool and a homogeneous solid is removed, which is then crushed by grinding. 100 g of this crushed material are then placed in a closable spherical shape with a volume of 100 cm3 and exposed to water vapor at 1,100 C for 60 minutes. You get after cooling and demolding a spherical porous molded body of the specific Weight O, I.

Claims (1)

PATENTANSPRUCH: Verfahren zur Herstellung maßhaltiger, poröser Formkörper aus zerkleinerten, thermoplastischen Kunststoffen in Gegenwart von Blähmitteln, dadurch gekennzeichnet, daß der zerkleinerte Kunststoff, der das Gas gelöst enthält, in nicht gasdicht schließende Formen eingebracht und dort durch Erwärmen auf Temperaturen oberhalb des Erweichungspunktes des Kunststoffes zu porösen Formkörpern versintert wird. PATENT CLAIM: Process for the production of dimensionally stable, porous moldings from shredded, thermoplastic plastics in the presence of blowing agents, characterized in that the crushed plastic, which contains the gas in dissolved form, placed in molds that do not close gas-tight and there by heating to temperatures sintered to form porous moldings above the softening point of the plastic will. In Betracht gezogene Druckschriften: Deutsche Patentschrift Nr. 38I 46I; belgische Patentschrift Nr. 496 635. Documents considered: German Patent No. 38I 46I; Belgian patent specification No. 496 635.
DEB14755A 1951-04-26 1951-04-27 Process for the production of dimensionally stable porous moldings from thermoplastics Expired DE973134C (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DEB14755A DE973134C (en) 1951-04-26 1951-04-27 Process for the production of dimensionally stable porous moldings from thermoplastics
US282682A US2779062A (en) 1951-04-26 1952-04-16 Production of porous shaped articles true to shape and size from synthetic thermoplastic materials
FR1055058D FR1055058A (en) 1951-04-26 1952-04-22 Process for the production of porous moldings of definite shapes from thermoplastics
GB10297/52A GB719729A (en) 1951-04-26 1952-04-24 Improvements in the production of porous shaped articles true to shape and size fromsynthetic thermoplastic materials

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE1055058X 1951-04-26
DE719729X 1951-04-26
DE2779062X 1951-04-26
DEB14755A DE973134C (en) 1951-04-26 1951-04-27 Process for the production of dimensionally stable porous moldings from thermoplastics

Publications (1)

Publication Number Publication Date
DE973134C true DE973134C (en) 1959-12-10

Family

ID=66428618

Family Applications (1)

Application Number Title Priority Date Filing Date
DEB14755A Expired DE973134C (en) 1951-04-26 1951-04-27 Process for the production of dimensionally stable porous moldings from thermoplastics

Country Status (4)

Country Link
US (1) US2779062A (en)
DE (1) DE973134C (en)
FR (1) FR1055058A (en)
GB (1) GB719729A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1158699B (en) * 1955-03-02 1963-12-05 Basf Ag Process for the production of small-scale, transparent thermoplastics
DE1261659B (en) * 1958-08-05 1968-02-22 Polymer Corp Method of making a porous nylon molded article
DE1629281B1 (en) * 1966-04-28 1972-03-23 Basf Ag Process for the production of foam-shaped moldings from olefin polymers
EP0447817A2 (en) * 1990-03-03 1991-09-25 BASF Aktiengesellschaft Process for preparing cellular polyurethane articles by sintering

Families Citing this family (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3126669A (en) * 1964-03-31 Whistling floating roly-poly toy
DE1002124B (en) * 1954-04-20 1957-02-07 Liselotte Sauer Process for the production of a sponge-like insulating material from polyamide textile waste
DE1017784B (en) * 1955-02-24 1957-10-17 Roehm & Haas Gmbh Process for the production of porous moldings consisting mainly of polymethacrylic acid methyl ester
US2885738A (en) * 1955-12-29 1959-05-12 Western Electric Co Methods of absorbing and retaining expanding media in plastic materials
US3020248A (en) * 1955-12-29 1962-02-06 Western Electric Co Method of making expandable plastic and preparation of cellular plastic therefrom
DE1183236B (en) * 1956-06-25 1964-12-10 Plastitect Ets Device for the production of porous molded bodies of low volume weight from strongly pre-foamed, still driftable polystyrene
US3035280A (en) * 1956-08-16 1962-05-22 Agricola Reg Trust Method of working expanded plastic and articles made by the method
US2857625A (en) * 1956-08-17 1958-10-28 Monsanto Chemicals Low density extruded styrene polymer foams
US2983570A (en) * 1958-02-10 1961-05-09 Pirelli Porous moulds for manufacturing plastic articles
US3017165A (en) * 1958-05-20 1962-01-16 Edward D Idzi Apparatus for aerating a liquid
US3015132A (en) * 1958-09-22 1962-01-02 Albert L Bunting Method of molding plastic articles
US2993604A (en) * 1959-05-12 1961-07-25 Matthew A Sullivan Display stand
US3018257A (en) * 1959-10-26 1962-01-23 American Cyanamid Co Method of preparing expandable resins comprising dissolving said resin in a miscibleblend of organic liquids
US3200175A (en) * 1960-06-17 1965-08-10 Crown Machine & Tool Company Method of making cups
US3137743A (en) * 1960-11-03 1964-06-16 Tru Scale Inc Method of forming foamed structures
US3183091A (en) * 1960-12-29 1965-05-11 Ibm Vesicular photographic film material and process for utilization of same
US3159875A (en) * 1961-06-30 1964-12-08 Springfield Cast Products Inc Automatic molding press
US3196484A (en) * 1961-09-01 1965-07-27 Dow Chemical Co Apparatus for continuous production of foamed plastic objects
US3208850A (en) * 1962-04-11 1965-09-28 Kalvar Corp Vesicular type photographic materials comprising a polyurethane resin containing light decomposable compounds
US3189455A (en) * 1962-04-30 1965-06-15 Kalvar Corp Vesicular photographic materials containing a polyamide vehicle
US3248464A (en) * 1962-08-22 1966-04-26 Dow Chemical Co Method and apparatus for making large celled material
US3661690A (en) * 1970-05-11 1972-05-09 Michael A Taranto Floatable washcloth
US3748464A (en) * 1972-02-08 1973-07-24 F Andeweg Wax shade
US3913298A (en) * 1972-06-29 1975-10-21 Grace W R & Co Method of packaging
US5271886A (en) * 1992-10-14 1993-12-21 Arco Chemical Technology, L.P. Process and apparatus for rapid pre-expension and molding of expandable polymer particles
EP1828268A4 (en) 2004-12-22 2009-01-14 Albemarle Corp Flame retardant polystyrene foam compositions
WO2006071213A1 (en) 2004-12-22 2006-07-06 Albemarle Corporation Flame retardant expanded polystyrene foam compositions
US9028730B2 (en) 2013-03-15 2015-05-12 Purolite Corporation Method of producing uniform polymer beads of various sizes
USD955392S1 (en) * 2020-03-18 2022-06-21 Smart Packaging Solutions Terminal for smart card
CN112549411B (en) * 2020-11-20 2022-03-11 美瑞新材料股份有限公司 Method and equipment for preparing foamed thermoplastic polyurethane shoe midsole

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE496635A (en) *
DE381461C (en) * 1923-09-20 Fritz Pfleumer Process for the production of hot-vulcanized foam from rubber or similar materials

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1534654A (en) * 1923-04-16 1925-04-21 Netz Glove & Mitten Co Filling for boxing gloves
US2200847A (en) * 1936-12-24 1940-05-14 Dunlop Rubber Co Process of vulcanizing sponge rubber
US2268160A (en) * 1939-06-21 1941-12-30 Du Pont Spongy superpolymer
US2447055A (en) * 1943-10-07 1948-08-17 Expanded Rubber Co Ltd Production of expanded plastic materials
US2363051A (en) * 1943-12-16 1944-11-21 Us Rubber Co Method of making cellular rubber
US2409910A (en) * 1944-11-29 1946-10-22 Dow Chemical Co Method of filling containers with resinous foam
US2531665A (en) * 1946-07-04 1950-11-28 Expanded Rubber Co Ltd Manufacture of expanded thermoplastic materials
US2524039A (en) * 1947-02-18 1950-10-03 Pascal J Carpentier Process of producing cellular rubber
US2525880A (en) * 1948-01-30 1950-10-17 Us Rubber Co Method of molding porous articles
US2602193A (en) * 1949-01-08 1952-07-08 United Shoe Machinery Corp Cellular resinous materials and processes of making the same
US2681321A (en) * 1950-02-27 1954-06-15 Basf Ag Production of porous materials from film-forming organic thermoplastic masses

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE496635A (en) *
DE381461C (en) * 1923-09-20 Fritz Pfleumer Process for the production of hot-vulcanized foam from rubber or similar materials

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1158699B (en) * 1955-03-02 1963-12-05 Basf Ag Process for the production of small-scale, transparent thermoplastics
DE1261659B (en) * 1958-08-05 1968-02-22 Polymer Corp Method of making a porous nylon molded article
DE1629281B1 (en) * 1966-04-28 1972-03-23 Basf Ag Process for the production of foam-shaped moldings from olefin polymers
EP0447817A2 (en) * 1990-03-03 1991-09-25 BASF Aktiengesellschaft Process for preparing cellular polyurethane articles by sintering
EP0447817A3 (en) * 1990-03-03 1992-03-18 Basf Aktiengesellschaft Process for preparing cellular polyurethane articles by sintering

Also Published As

Publication number Publication date
US2779062A (en) 1957-01-29
FR1055058A (en) 1954-02-16
GB719729A (en) 1954-12-08

Similar Documents

Publication Publication Date Title
DE973134C (en) Process for the production of dimensionally stable porous moldings from thermoplastics
DE953835C (en) Process for the production of porous moldings from thermoplastics
DE1004372B (en) Propellant for the production of foam bodies
US3859404A (en) Densifying plastic foam scrap
DE2846620B1 (en) Process for producing polyolefin-based foams
DE1504674B1 (en) Process for the continuous production of objects from hard foam on the basis of polyvinyl chloride containing polyisocyanates by extrusion
DE1243872B (en) Production of foam plastics from polyesters and polycarbonates
DE2152793B2 (en) Process for the production of a freeze-dried coffee extract powder with a bulk density of 200 to 250 g / l and the color of ground coffee
DE1629296A1 (en) Process for the production of closed cell foam particles
DE956808C (en) Process for the production of porous moldings from thermoplastics
DE249777C (en)
DE970725C (en) Insulating body, consisting of crushed cork treated with a binding agent, and a method for producing such an insulating body
DE1174969B (en) Process and device for the production of bulky thermoplastic plastics in small-scale form
DE831319C (en) Propellant for the production of molded parts with a porous or sponge-like structure
DE951299C (en) Process for introducing liquid blowing agents into styrene polymers
DE923390C (en) Process for the production of cellular rubber molded articles
DE1261670B (en) Process for the continuous production of cell bodies from polymers of vinyl chloride or vinyl aromatic monomers
DE1009391B (en) Process for the production of blowing agent-containing styrene polymers
AT204785B (en) Process for the production of rigid, porous, thermoplastic materials
AT232716B (en) Process for the production of hollow bodies from foamed thermoplastics using the centrifugal casting process
US2086513A (en) Expanded rubber
DE1769861B2 (en) Process for the production of foamed chlorinated polyethylene
DE1151923B (en) Process for the production of foam plastic bodies with the admixture of shredded foam plastic waste on a polystyrene basis and a device for shredding waste
DE1911395C3 (en) Process for the production of foamed elastic moldings
AT256472B (en) Process for the production of shaped objects with a substantially closed cell structure from thermoplastic material